CN107519790A - A kind of liquid mixing system - Google Patents

A kind of liquid mixing system Download PDF

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Publication number
CN107519790A
CN107519790A CN201610449064.9A CN201610449064A CN107519790A CN 107519790 A CN107519790 A CN 107519790A CN 201610449064 A CN201610449064 A CN 201610449064A CN 107519790 A CN107519790 A CN 107519790A
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CN
China
Prior art keywords
pipe
valve
diaphragm valve
pipeline
agitation tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201610449064.9A
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Chinese (zh)
Inventor
罗厚友
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hubei Hengfeng Medical Pharmaceutical Equipment Co Ltd
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Hubei Hengfeng Medical Pharmaceutical Equipment Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hubei Hengfeng Medical Pharmaceutical Equipment Co Ltd filed Critical Hubei Hengfeng Medical Pharmaceutical Equipment Co Ltd
Priority to CN201610449064.9A priority Critical patent/CN107519790A/en
Publication of CN107519790A publication Critical patent/CN107519790A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/90Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms 
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/181Preventing generation of dust or dirt; Sieves; Filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/83Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
    • B01F35/832Flow control by weighing

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Apparatus For Disinfection Or Sterilisation (AREA)

Abstract

A kind of liquid mixing system, there is Agitation Tank, Agitation Tank outer wall is provided with chuck, and Agitation Tank is provided with charging aperture, ingredients mouth, Butterworth Hatch, pure steam entrance, pure air entrance and discharging opening, agitating device and cleaning device are set in Agitation Tank;The external proportioner of ingredients mouth;Cleaning device, external cleaning liquid device is inscribed in Butterworth Hatch;The external pure steam generating means of pure steam entrance;The external pure air generating means of pure air entrance, and ball valve D1, air cleaner and manual diaphragm valve J2 are sequentially connected in series on pipeline, air cleaner arranges blast pipe A, pneumatic diaphragm valve F5, F6 are in series with blast pipe A, the pipeline of air cleaner inlet end is provided with the blast pipe A between branch pipe A connection pneumatic diaphragm valves F5, F6, and the discharge outlet of air cleaner connects the blast pipe A of the pneumatic diaphragm valve F6 other ends by ball valve D2 with branch pipe B;The present invention is simple to operate, equipment cost is low, Disinfection Effect is good, realizes manual/auto control.

Description

A kind of liquid mixing system
Technical field
The present invention is a kind of liquid mixing system, is related to the material configuration of the industry such as bioengineering, big transfusion, oral liquid, fine chemistry.
Background technology
Currently, liquid mixing system is widely used in the material configuration of the industry such as bioengineering, big transfusion, oral liquid, fine chemistry, effectively eliminates cross pollution and product microbiological contamination equivalent risk in configuration process, improves the production efficiency and reliability of product.
Existing liquid mixing system has Agitation Tank, Agitation Tank outer wall is provided with chuck, chuck is used to Agitation Tank be heated or cooled, charging aperture, ingredients mouth, Butterworth Hatch, pure steam entrance, pure air entrance and discharging opening are provided with Agitation Tank, agitating device and cleaning device are provided with Agitation Tank, wherein agitating device has stirring motor, the axle stretch end of stirring motor is equipped with rotating shaft, rotating shaft is located in Agitation Tank, turn the tip of the axis and blade for stirring is installed, and ingredients mouth docks proportioner by pipeline(Inject water installations), Butterworth Hatch is docked by pipeline cleans liquid device, and pure steam entrance docks pure steam generating means by pipeline, and pure air entrance docks pure steam generating means by pipeline, and air cleaner is housed on pipeline.However, there is problems with existing liquid mixing system:(1) need separately to set exhaust outlet on Agitation Tank, and air cleaner is installed on the pipeline of exhaust outlet peripheral hardware, to be filtered to discharging gas in Agitation Tank, this significantly increases equipment cost;(2) cleaning of existing liquid mixing system, sterilization process are poor, it is impossible to accomplish to each pipeline, sterilization especially to discharge nozzle, blow-off pipe and blast pipe, remaining water and drying process are blown, to reduce bacterium residual to greatest extent;(3) existing liquid mixing system can only be completed to operate accordingly by valve event corresponding to the manual control of each control button, it is impossible to accomplish Automated condtrol, so as to complex operation, labor intensity is big, and production cost is high, and dispensing accuracy is low.
The content of the invention
It is high present invention aim to solve current liquid mixing system equipment cost, cleaning, sterilization process are poor, and it can only control manually, complex operation, the problem of labor intensity is big, and production cost is high, and dispensing accuracy is low, for a kind of this cost is low, Disinfection Effect is good, the liquid mixing system of manual/auto control is realized.
The present invention concrete scheme be:A kind of liquid mixing system, with Agitation Tank, Agitation Tank outer wall is provided with chuck, and chuck is used to Agitation Tank be heated or cooled, charging aperture, ingredients mouth, Butterworth Hatch, pure steam entrance, pure air entrance and discharging opening are provided with Agitation Tank, agitating device and cleaning device are provided with Agitation Tank;It is characterized in that:Manual diaphragm valve J1 is housed on the external pipeline of charging aperture;Ingredients mouth connects proportioner by pneumatic diaphragm valve F1 with external pipeline;Cleaning device is inscribed in Butterworth Hatch, and connects cleaning liquid device with external pipeline by pneumatic diaphragm valve F2;Pure steam entrance connects pure steam generating means by pneumatic diaphragm valve F3, F4 and external pipeline;Pure air entrance connects pure air generating means by external pipeline, and ball valve D1, air cleaner and manual diaphragm valve J2 are sequentially connected in series on pipeline, wherein air cleaner arranges blast pipe A, pneumatic diaphragm valve F5, F6 are in series with blast pipe A, the blast pipe A being provided with the pipeline of air cleaner inlet end between branch pipe A connection pneumatic diaphragm valves F5, F6, the discharge outlet of air cleaner connect the blast pipe A of the pneumatic diaphragm valve F6 other ends by ball valve D2 with branch pipe B;Manual diaphragm valve J3 is housed in discharging opening, and is provided with external discharge nozzle, blow-off pipe and blast pipe B, wherein discharge nozzle, blow-off pipe are corresponding with blast pipe B is equipped with manual diaphragm valve J4, ball valve D3 and ball valve D4;Described pneumatic diaphragm valve F1, F2~F6 unlatching/closing and the operation of agitating device are controlled by corresponding control button respectively.
Heretofore described chuck is provided with upper and lower fairlead, and upper fairlead is connected to steam outlet pipe, normal air enters pipe and cooling water outlet tube, and enters to correspond on pipe and cooling water outlet tube in steam outlet pipe, normal air and pneumatic stopping valve X1, X2, X3 are housed;Lower fairlead connects steam and enters pipe, drainpipe and cooling water respectively enters pipe, wherein drainpipe connection blast pipe A, and pneumatic stopping valve X4 and steam trap have been sequentially connected in series on drainpipe;Steam enters pipe connection blow-off pipe, and enters pneumatic stopping valve X5 is housed on pipe in steam;Enter in cooling water and pneumatic stopping valve X6 is housed on pipe;Described pneumatic stopping valve X1, X2~X6 control its unlatching/closing by corresponding control button respectively.
Bypass branch A is provided with pipeline in the present invention between pneumatic diaphragm valve F3, F4, manual diaphragm valve J5 is housed on bypass branch A;Bypass branch B is provided with the pipeline of air cleaner outlet side, manual diaphragm valve J6 is housed on bypass branch B;Air bleeding valve J7 is equipped in manual diaphragm valve J3 side;The bypass branch A communicates with the bypass branch B other end, and connects air bleeding valve J7 by pipeline.
Equipped with safety valve S1 and pressure sensor P2 on the upper fairlead of chuck in the present invention;Pressure sensor P3 is housed on the external pipeline where pure air generating means to ball valve D1;Temperature sensor T2 is housed on blast pipe A;In Agitation Tank built with pressure sensor P1, temperature sensor T1 and liquid level sensor L1;Angular-rate sensor W1 is housed in the rotating shaft of agitating device;Pressure sensor P1~the P3, temperature sensor T1~T2, liquid level sensor L1 and angular-rate sensor W1 communicate connection PLC respectively, PLC communication connection touch-screen, and realize the real-time control for the operation that works pneumatic diaphragm valve F1, F2~F6 and pneumatic stopping valve X1, X2~X6 unlatching/closing and agitating device.
The present invention has advantages below:
(1) present invention is simple in construction, ingenious in design, realizes the filtering for the pure air being passed through to Agitation Tank in discharging simultaneously by using an air cleaner and Agitation Tank discharges the filtering of gas after dispensing is completed in tank, greatly reduce equipment cost.
(2) present invention realizes the sterilization to discharge nozzle, blow-off pipe and blast pipe, blows remaining water and drying process, to reduce pipe Endophytic bacteria residual to greatest extent, effectively prevent cross pollution by designing bypass branch A, B and air bleeding valve J7.
(3) present invention can not only realize the manual control to liquid mixing system, and realize the dispensing to liquid mixing system, discharging, cleaning and the real-time monitoring for sterilizing parameters in the Automated condtrol and blending process of these processes, it is so simple to operate, operating cost is greatly reduced, improves the accuracy of dispensing.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention;
Fig. 2 is the control structure block diagram of the present invention.
In figure:1-Agitation Tank,2-chuck,3-charging aperture,4-ingredients mouth,5-Butterworth Hatch,6-pure steam entrance,7-pure air entrance,8-discharging opening,9-agitating device,10-cleaning device,11-proportioner,12-cleaning liquid device,13-pure steam generating means,14-pure air generating means,15-air cleaner,16-blast pipe A,17-branch pipe A,18-branch pipe B,19-discharge nozzle,20-blow-off pipe,21-blast pipe B,22-go up fairlead,23-lower fairlead,24-steam outlet pipe,25-normal air enters pipe,26-cooling water outlet tube,27-steam enters pipe,28-drainpipe,29-cooling water enters pipe,30-steam trap,31-bypass branch A,32-bypass branch B,33-PLC,34-touch-screen,35-Weighing module.
Embodiment
Referring to Fig. 1, the present invention has Agitation Tank 1, the outer wall of Agitation Tank 1 is provided with chuck 2, chuck 2 is used to Agitation Tank 1 be heated or cooled, charging aperture 3, ingredients mouth 4, Butterworth Hatch 5, pure steam entrance 6, pure air entrance 7 and discharging opening 8 are provided with Agitation Tank 1, agitating device 9 and cleaning device 10 are provided with Agitation Tank 1;Particularly:Manual diaphragm valve J1 is housed on the external pipeline of charging aperture 3;Ingredients mouth 4 connects proportioner 11 with external pipeline by pneumatic diaphragm valve F1;Cleaning device 10 is inscribed in Butterworth Hatch 5, and connects cleaning liquid device 12 with external pipeline by pneumatic diaphragm valve F2;Pure steam entrance 6 connects pure steam generating means 13 by pneumatic diaphragm valve F3, F4 and external pipeline;Pure air entrance 7 connects pure air generating means 14 by external pipeline, and ball valve D1, air cleaner 15 and manual diaphragm valve J2 are sequentially connected in series on pipeline, wherein air cleaner 15 arranges blast pipe A16, pneumatic diaphragm valve F5, F6 are in series with blast pipe A16, the blast pipe A16 being provided with the pipeline of the inlet end of air cleaner 15 between branch pipe A17 connection pneumatic diaphragm valves F5, F6, the discharge outlet of air cleaner 15 connect the blast pipe A16 of the pneumatic diaphragm valve F6 other ends by ball valve D2 with branch pipe B18;Manual diaphragm valve J3 is housed in discharging opening 8, and provided with external discharge nozzle 19, blow-off pipe 20 and blast pipe B21, wherein discharge nozzle 19, blow-off pipe 20 are corresponding with blast pipe B21 is equipped with manual diaphragm valve J4, ball valve D3 and ball valve D4;Described pneumatic diaphragm valve F1, F2~F6 unlatching/closing and the operation of agitating device 9 are controlled by corresponding control button respectively.
Chuck 2 described in the present embodiment is provided with upper and lower fairlead 22,23, upper fairlead 22 is connected to steam outlet pipe 24, normal air enters pipe 25 and cooling water outlet tube 26, and enters to correspond on pipe 25 and cooling water outlet tube 26 in steam outlet pipe 24, normal air and pneumatic stopping valve X1, X2, X3 are housed;Lower fairlead 23 connects steam and enters pipe 27, drainpipe 28 and cooling water respectively enters pipe 29, and wherein drainpipe 28 connects blast pipe A16, and pneumatic stopping valve X4 and steam trap 30 have been sequentially connected in series on drainpipe 28;Steam enters pipe 27 and connects blow-off pipe 20, and enters pneumatic stopping valve X5 is housed on pipe 27 in steam;Enter in cooling water and pneumatic stopping valve X6 is housed on pipe 29;Described pneumatic stopping valve X1, X2~X6 control its unlatching/closing by corresponding control button respectively.
Bypass branch A31 is provided with pipeline in the present embodiment between pneumatic diaphragm valve F3, F4, manual diaphragm valve J5 is housed on bypass branch A31;Bypass branch B32 is provided with the pipeline of the outlet side of air cleaner 15, manual diaphragm valve J6 is housed on bypass branch B32;Air bleeding valve J7 is equipped in manual diaphragm valve J3 side;The bypass branch A31 communicates with the bypass branch B32 other end, and connects air bleeding valve J7 by pipeline.
Referring to Fig. 2, equipped with safety valve S1 and pressure sensor P2 on the upper fairlead 22 of chuck 2 in the present embodiment;Pressure sensor P3 is housed on the external pipeline where pure air generating means 14 to ball valve D1;Temperature sensor T2 is housed on blast pipe A16;In Agitation Tank 1 built with pressure sensor P1, temperature sensor T1 and liquid level sensor L1;Angular-rate sensor W1 is housed in the rotating shaft of agitating device 9;Pressure sensor P1~the P3, temperature sensor T1~T2, liquid level sensor L1 and angular-rate sensor W1 communicate connection PLC 33 respectively(Pressure sensor P1~P3 is alternatively pressure gauge, and temperature sensor T1~T2 is alternatively thermometer), the communication connection touch-screen 34 of PLC 33, and realize the real-time control of the unlatching/closing and the work operation of agitating device 9 to pneumatic diaphragm valve F1, F2~F6 and pneumatic stopping valve X1, X2~X6.
Below by taking the real-time control of unlatching/closing of the PLC to each pneumatic diaphragm valve and pneumatic stopping valve as an example, the specific work process of the present invention is described:
(1) feed:Manually opened manual diaphragm valve J1, added materials from charging aperture 3 into Agitation Tank 1, now agitating device 9 starts startup optimization, pneumatic stopping valve X3, X6 are opened, cooling water enters from the lower fairlead 23 of chuck 2, is discharged from upper fairlead 22, Agitation Tank 1 is cooled;
(2) dispensing:Pneumatic diaphragm valve F1 is opened, injection water in proportioner 11 is entered in Agitation Tank 1 along pipeline from ingredients mouth 4, the now pressure sensor P1 in Agitation Tank 1, temperature sensor T1, liquid level sensor L1 is in real time by the air pressure in the tank body monitored, feed temperature is transferred to PLC 33 with liquid level data, the data that PLC 33 monitors according to angular-rate sensor W1 in real time control the mixing speed of agitating device 9, when the Weighing module 35 of peripheral hardware detects that the current weight of Agitation Tank 1 reaches requirement, PLC 33 controls pneumatic diaphragm valve F1 to close, proportioner 11 stops adding injection water into Agitation Tank 1;
(3) discharge:Manual unlocking ball valve D1, manual diaphragm valve J2, J3, J4, pure air generating means 14 is passed through pure air into Agitation Tank 1 along pipeline by air cleaner 15 and pure air entrance 7, and the liquid configured in Agitation Tank 1 is discharged from discharge nozzle 19 under the influence of air pressure;
(4) clean:Pneumatic diaphragm valve F2 is opened, cleaning fluid caused by cleaning liquid device 12 is entered in Agitation Tank 1 along pipeline from Butterworth Hatch 5, and carries out internal washing to Agitation Tank 1 by cleaning device 10, after the completion of to be cleaned, manually opened manual diaphragm valve J3 and ball valve D3, sewage is discharged from blow-off pipe 20 in tank;
(5) Yu Shui is blown:(a) ball valve D2 is opened, the condensed water in air cleaner 15 passes sequentially through ball valve D2, branch pipe B18 and blast pipe A16 discharges;Manually opened ball valve D1, pneumatic diaphragm valve F6 are opened, and the pure air that the conveying of pure air generating means 14 comes passes sequentially through ball valve D1, branch pipe A17 and pneumatic diaphragm valve F6 and the remaining water in blast pipe A16 is purged;(b) manually opened ball valve D1, manual diaphragm valve J6, J7, and manual diaphragm valve J4, ball valve D3, ball valve D4 are opened in selection successively, pure air generating means 14 conveys the pure air to come after the filtering of air cleaner 15, realizes successively and discharge nozzle 19, blow-off pipe 20 and the remaining water in blast pipe B21 are purged;
(6) sterilize:(a) tank body is sterilized:Pneumatic diaphragm valve F3, F4 are opened, and the pure steam that the conveying of pure steam generating means 13 comes passes sequentially through pneumatic diaphragm valve F3, F4 along pipeline and pure air entrance 6 is entered in Agitation Tank 1, and the bacterium in tank body is carried out disinfection using high temperature;(b) filter core of air cleaner 15 is carried out disinfection:Manually opened manual diaphragm valve J2, pneumatic diaphragm valve F5 are opened, pure steam in tank body passes sequentially through manual diaphragm valve J2, the filter core of air cleaner 15 and branch pipe A17 along pipeline, and pass through pneumatic diaphragm valve F5, finally discharged from blast pipe A16, so as to reach the purpose to be carried out disinfection to the filter core of air cleaner 15;(c) discharge nozzle 19, blow-off pipe 20 and blast pipe B21 are carried out disinfection:Manually opened manual diaphragm valve J2, J6, J7, and unlatching manual diaphragm valve J4, ball valve D3, ball valve D4 are selected successively, the pure steam in tank body realizes the high-temperature sterilization to discharge nozzle 19, blow-off pipe 20 and blast pipe B21 along pipeline successively;
(7) processing is dried to Agitation Tank 1:(a) pneumatic stopping valve X3, X6 is closed, and pneumatic stopping valve X2, X4 are opened, and is passed through air into chuck 2 into 25 by normal air, the cooling water in chuck 2 is discharged along lower fairlead 23 and drainpipe 28 under the influence of air pressure;(b) pneumatic diaphragm valve F3 and pneumatic stopping valve X1, X5 are opened, and manually opened manual diaphragm valve J5, J7 and ball valve D3, pure steam generating means 13 convey the pure steam that comes along Pipeline transport to chuck 2 in, and discharged by upper fairlead 22 and steam outlet pipe 24, it is achieved thereby that being heated to the tank skin of Agitation Tank 1, and reach in the presence of heat transfer to the withering purpose of tank interior;(c) manual unlocking manual diaphragm valve J3 and ball valve D3, the interior condensed water condensed of venting Agitation Tank 1.

Claims (4)

  1. A kind of 1. liquid mixing system, with Agitation Tank, Agitation Tank outer wall is provided with chuck, and chuck is used to Agitation Tank be heated or cooled, charging aperture, ingredients mouth, Butterworth Hatch, pure steam entrance, pure air entrance and discharging opening are provided with Agitation Tank, agitating device and cleaning device are provided with Agitation Tank;It is characterized in that:Manual diaphragm valve J1 is housed on the external pipeline of charging aperture;Ingredients mouth connects proportioner by pneumatic diaphragm valve F1 with external pipeline;Cleaning device is inscribed in Butterworth Hatch, and connects cleaning liquid device with external pipeline by pneumatic diaphragm valve F2;Pure steam entrance connects pure steam generating means by pneumatic diaphragm valve F3, F4 and external pipeline;Pure air entrance connects pure air generating means by external pipeline, and ball valve D1, air cleaner and manual diaphragm valve J2 are sequentially connected in series on pipeline, wherein air cleaner arranges blast pipe A, pneumatic diaphragm valve F5, F6 are in series with blast pipe A, the blast pipe A being provided with the pipeline of air cleaner inlet end between branch pipe A connection pneumatic diaphragm valves F5, F6, the discharge outlet of air cleaner connect the blast pipe A of the pneumatic diaphragm valve F6 other ends by ball valve D2 with branch pipe B;Manual diaphragm valve J3 is housed in discharging opening, and is provided with external discharge nozzle, blow-off pipe and blast pipe B, wherein discharge nozzle, blow-off pipe are corresponding with blast pipe B is equipped with manual diaphragm valve J4, ball valve D3 and ball valve D4;Described pneumatic diaphragm valve F1, F2~F6 unlatching/closing and the operation of agitating device are controlled by corresponding control button respectively.
  2. 2. a kind of liquid mixing system according to claim 1, it is characterized in that:The chuck is provided with upper and lower fairlead, and upper fairlead is connected to steam outlet pipe, normal air enters pipe and cooling water outlet tube, and enters to correspond on pipe and cooling water outlet tube in steam outlet pipe, normal air and pneumatic stopping valve X1, X2, X3 are housed;Lower fairlead connects steam and enters pipe, drainpipe and cooling water respectively enters pipe, wherein drainpipe connection blast pipe A, and pneumatic stopping valve X4 and steam trap have been sequentially connected in series on drainpipe;Steam enters pipe connection blow-off pipe, and enters pneumatic stopping valve X5 is housed on pipe in steam;Enter in cooling water and pneumatic stopping valve X6 is housed on pipe;Described pneumatic stopping valve X1, X2~X6 control its unlatching/closing by corresponding control button respectively.
  3. 3. a kind of liquid mixing system according to claim 1, it is characterized in that:Bypass branch A is provided with pipeline between pneumatic diaphragm valve F3, F4, manual diaphragm valve J5 is housed on bypass branch A;Bypass branch B is provided with the pipeline of air cleaner outlet side, manual diaphragm valve J6 is housed on bypass branch B;Air bleeding valve J7 is equipped in manual diaphragm valve J3 side;The bypass branch A communicates with the bypass branch B other end, and connects air bleeding valve J7 by pipeline.
  4. 4. a kind of liquid mixing system according to claim 2, it is characterized in that:Equipped with safety valve S1 and pressure sensor P2 on the upper fairlead of chuck;Pressure sensor P3 is housed on the external pipeline where pure air generating means to ball valve D1;Temperature sensor T2 is housed on blast pipe A;In Agitation Tank built with pressure sensor P1, temperature sensor T1 and liquid level sensor L1;Angular-rate sensor W1 is housed in the rotating shaft of agitating device;Pressure sensor P1~the P3, temperature sensor T1~T2, liquid level sensor L1 and angular-rate sensor W1 communicate connection PLC respectively, PLC communication connection touch-screen, and realize the real-time control for the operation that works pneumatic diaphragm valve F1, F2~F6 and pneumatic stopping valve X1, X2~X6 unlatching/closing and agitating device.
CN201610449064.9A 2016-06-21 2016-06-21 A kind of liquid mixing system Pending CN107519790A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610449064.9A CN107519790A (en) 2016-06-21 2016-06-21 A kind of liquid mixing system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610449064.9A CN107519790A (en) 2016-06-21 2016-06-21 A kind of liquid mixing system

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Publication Number Publication Date
CN107519790A true CN107519790A (en) 2017-12-29

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108079864A (en) * 2018-02-05 2018-05-29 贵州黔钟科技有限公司 Enzyme cleaning solution automatic proportioner
CN108311010A (en) * 2018-01-05 2018-07-24 苏州浙远自动化工程技术有限公司 Automatic liquid thermal preparation device and method
CN108548695A (en) * 2018-02-09 2018-09-18 浙江中控系统工程有限公司 A kind of automatic sampling system being suitable for medicine bioengineering reactor and its application
CN109317011A (en) * 2018-11-14 2019-02-12 滁州天鼎丰非织造布有限公司 Automatically match colloid system
CN113426596A (en) * 2021-07-14 2021-09-24 连云港宝畅流体输送设备有限公司 Automatic cloth system of liquid seasoning
CN113559776A (en) * 2021-09-02 2021-10-29 无锡维邦工业设备成套技术有限公司 Apparatus for producing of purified water configuration antiseptic solution
CN114618361A (en) * 2022-03-16 2022-06-14 南京百帕斯制药设备科技有限公司 Full-automatic aseptic liquid preparation system
CN115253841A (en) * 2022-08-02 2022-11-01 江苏谷地机械科技有限公司 Full-automatic traditional Chinese medicine oral liquid production and safety management system

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108311010A (en) * 2018-01-05 2018-07-24 苏州浙远自动化工程技术有限公司 Automatic liquid thermal preparation device and method
CN108311010B (en) * 2018-01-05 2021-06-08 苏州浙远自动化工程技术有限公司 Automatic liquid thermal preparation device and method
CN108079864A (en) * 2018-02-05 2018-05-29 贵州黔钟科技有限公司 Enzyme cleaning solution automatic proportioner
CN108548695A (en) * 2018-02-09 2018-09-18 浙江中控系统工程有限公司 A kind of automatic sampling system being suitable for medicine bioengineering reactor and its application
CN109317011A (en) * 2018-11-14 2019-02-12 滁州天鼎丰非织造布有限公司 Automatically match colloid system
CN113426596A (en) * 2021-07-14 2021-09-24 连云港宝畅流体输送设备有限公司 Automatic cloth system of liquid seasoning
CN113559776A (en) * 2021-09-02 2021-10-29 无锡维邦工业设备成套技术有限公司 Apparatus for producing of purified water configuration antiseptic solution
CN114618361A (en) * 2022-03-16 2022-06-14 南京百帕斯制药设备科技有限公司 Full-automatic aseptic liquid preparation system
CN115253841A (en) * 2022-08-02 2022-11-01 江苏谷地机械科技有限公司 Full-automatic traditional Chinese medicine oral liquid production and safety management system

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Application publication date: 20171229